Kinetics of Reduction of Aqueous Hexaammineruthenium(III) Ion at Pt

Article pubs.acs.org/IC

Kinetics of Reduction of Aqueous Hexaammineruthenium(III) Ion at Pt and Au Microelectrodes: Electrolyte, Temperature, and Pressure Effects Vijendran Vijaikanth,† Guangchun Li, and Thomas W. Swaddle* Department of Chemistry, University of Calgary, Calgary, Alberta, Canada T2N 1N4

Inorg. Chem. 2013.52:2757-2768. Downloaded from pubs.acs.org by UNIV OF WINNIPEG on 01/23/19. For personal use only.

S Supporting Information *

ABSTRACT: Rate constants kel obtained by impedance spectroscopy for the reduction of Ru(NH3)63+ at polycrystalline Pt and Au ultramicroelectrodes depend strongly on the identity and concentration of the anion present in the order CF3SO3− < Cl− < ClO4−, but not on the cation of the supporting electrolyte (Na+, K+, H+). For Cl− as the sole anion present, kel is directly proportional to the total [Cl−], such that kel would be zero if Cl− were hypothetically absent, indicating that Cl− is directly involved in mediation of the Ru(NH3)63+/2+ electron transfer. For CF3SO3− as the sole counterion, the dependence of kel on the total [CF3SO3−] is not linear, possibly because blocking of the available electrode surface becomes dominant at high triflate concentrations. Volumes of activation ΔVel⧧ for reduction of Ru(NH3)63+ at an electrode in presence of Cl− or CF3SO3− are much more negative than predictions based on theory (Swaddle, T. W. Chem. Rev. 2005, 105, 2573) that has been successful with other electron transfer reactions but which does not take into account the involvement of the anions in the activation process. The strongly negative ΔVel⧧ values probably reflect solvation increases peculiar to activation processes of RuIII/II am(m)ine complexes, possibly together with promotion of desorption of surfaceblocking Cl− or CF3SO3− from electrodes by applied pressure. Frumkin corrections for Ru(NH3)63+ within the diffuse double layer would make ΔVel⧧ even more negative than is observed, although the corrections would be small. The strongly negative ΔVel⧧ values are inconsistent with reduction of Ru(NH3)63+ in direct contact with the metallic electrode surface, which would entail substantial dehydration of both the electrode and Ru(NH3)63+. Reduction of Ru(NH3)63+ can be regarded as taking place in hard contact with adsorbed water at the outer Helmholtz plane.

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−RT(∂ ln kel/∂P)T) for an electrode reaction that is likely to be close to fully adiabatic. Only aqueous systems are considered, since solvent dynamics can determine ΔVel⧧ for electrode processes in nonaqueous media.1 The question of the extent of nonadiabaticity in electrode reactions is controversial. The reduction of quinones at graphite electrodes is the subject of a current debate4,5 in which Compton et al.4 favor a nonadiabatic interpretation. For reductions of other organic solutes at electrodes in nonaqueous solvents, Savéant6 has derived a variant of the classical Marcus− Hush relationship which allows description of the passage from nonadiabatic to limiting adiabatic electron transfer. In a similar vein, Compton et al.7,8 have estimated the degree of adiabaticity and the changeover between nonadiabatic and limiting adiabatic behavior for electroreduction of 3-nitrophenolate and 1-nitropentane at Hg microhemispheres in organic solvents, using an asymmetric version of Marcus−Hush theory to interpret the pre-exponential factor in the temperature dependence of kel. For reductions of aqueous inorganic solutes at solid metal electrodes, it is typically assumed that the rate

INTRODUCTION Research in our laboratory in recent years has focused on mechanistic insights provided by the effects of hydrostatic pressure on the rates of heterogeneous (electrode) and homogeneous electron transfer reactions of transition-metal complexes in solution.1,2 Electrode reaction rates, however, are notoriously susceptible to the influence of the nature of the electrode surface. Although electron transfer at metal electrodes is traditionally viewed as adiabatic, we have suggested1 that in many cases this sensitivity to the state of the surface probably reflects nonadiabatic electron transfer (i.e., coupling between the electronic wave functions in the reactant and the electrode is weak relative to thermal energies3), so that the electrode reaction rate becomes strongly distance dependent and consequently sensitive to adsorbed substances, oxides layers, and so forth on the electrode surface. The standard techniques of electrode kinetics at conventional electrodes used heretofore in variable-pressure studies, notably ac voltammetry (ACV), are limited to moderately slow reactions having standard rate constant kel less than about 0.3 cm s−1, the slowness of which may indicate substantial departure from adiabaticity. We have therefore sought information on the pressure dependence of kel (conveniently expressed as the volume of activation ΔVel⧧ = © 2013 American Chemical Society

Received: January 10, 2013 Published: February 19, 2013 2757

dx.doi.org/10.1021/ic400062b | Inorg. Chem. 2013, 52, 2757−2768

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constant should be substantially independent of the nature of the metalin the present study, Au vs Ptif the reaction is fully adiabatic;9 for a nonadiabatic process, kel would depend on the density ρF of electronic states at the Fermi level of the electrode as well as on the electrode-reactant distance. Gosavi and Marcus,10 however, point out that kel can also be approximately the same at Pt and Au for a nonadiabatic reaction if a large ρF, as is typical for d bands as in Pt, is offset by the weaker coupling of d bands to the reactant relative to s bands as in Au. Thus, even if kel for a particular reaction is approximately the same at Au and Pt electrodes, the reaction is not necessarily adiabatic. As far as the variable-pressure studies reported here are concerned, nonadiabaticity will affect kel but probably not ΔVel⧧.11,12 As remarked originally by Gennett and Weaver,13 the lowspin/low-spin (t2g5/t2g6) Ru(NH3)63+/2+ electron transfer reaction, in which the Ru−N bond length difference between the effectively substitution-inert reactants (4.0 pm)14 and consequently the internal reorganization energy are very small, is likely to be a fast, “well-behaved”, adiabatic reaction. The Ru(NH3)63+/2+ couple has therefore come to be widely regarded as an electrochemical “reference reaction”, whether the electrode material be metallic,13,15−23 metallic with adsorbed monolayers,20,24−36 pyrolytic graphite,37−41 glassy carbon,42 or boron-doped diamond.43,44 For all these electrodes, it emerges that the Ru(NH3)63+/2+ couple is free of most of the aberrations associated with the Fe(CN)63−/4− couple,1,24,39−44 traditionally used as a reference system in electrode kinetics. For metallic electrodes, the reported Ru(NH3)63+/2+ electron transfer rates are very fast, albeit somewhat scattered for reasons discussed below, and in most cases appear to be roughly independent of the metal of the electrode, consistent with substantially adiabatic election transfer.9 Velmurugan et al.,45 however, found somewhat higher rates of reduction of Ru(NH3)63+ at Pt than at Au disk nanoelectrodes in various electrolyte solutions, and suggested some degree of nonadiabaticity, so this remains an open question. Successful measurements of the high kel values for the Ru(NH3)63+/2+ electrode reaction were made by Gennett and Weaver13 using ac voltammetry at a dropping Hg electrode, and were soon followed by those of Iwasita et al.15,16 using various ring electrodes in turbulent pipe flow. In many of the early reports, however, it is unclear whether the uncompensated resistance of the solutions had been adequately allowed for in deriving kel values.46 For convenient adaptation to high pressure experiments, we chose to study the Ru(NH3)63+/2+ electrode kinetics by ac impedance measurements at Pt and Au ultramicroelectrodes, as used by Muzikár ̌ and Fawcett22,23 in their studies of this system in dilute HClO4 media at 25 °C. Oxidizing anions such as perchlorate and nitrate, however, are usually avoided in Ru ammine chemistry because of the risk of oxidation of Ru(NH3)63+ and especially Ru(NH3)62+;47,48 this is unlikely to have been significant in the work of Muzikár ̌ and Fawcett because of the evidently short time-scales of their experiments, the moderate concentrations of ClO4−, and the merely transient presence of Ru(NH3)62+. In our study, the variable-pressure and -temperature experiments extended over several hours, and therefore only chloride and trifluoromethanesulfonate (triflate) media and Ru(NH3)63+ salts were used in them; no attempt was made to isolate solid [Ru(NH3)6](ClO4)3 as it is of limited solubility24 and is potentially explosive.

Article

EXPERIMENTAL SECTION

Fabrication of Ultramicroelectrodes (UMEs). Gold (⌀ 12.7 μm, 99.9%; ⌀ 25 μm, 99.95%) and Pt (⌀ 25 μm, 99.95%; ⌀ 10 μm, 99.95%) wires were obtained from Alfa Aesar. The wires were soldered to Cu connecting wire and then sealed in soft glass tubes by melting the latter cautiously in a Bunsen flame. The other end was closed with an insulating epoxy resin. Then the uniform microelectrode surface was exposed by grinding the tip with fine sandpaper (1500 grade) followed by polishing in a suspension of 0.05 μm alumina. For the high pressure work, the Au (⌀ 25 μm) and Pt (⌀ 25 μm) electrodes were constructed from polypropylene micropipet tips by melting the latter cautiously with an ethanol flame. The ends of the micropipet tips were then cut off squarely to expose a disk UME. The remainder of the tip was trimmed down and glued to the electrode holder with an insulating epoxy resin. The integrity of the UME disks and seals as checked with an optical microscope. The UME faces were polished with an aqueous suspension of 0.05 mm alumina, sonicated briefly in a K2S2O8/H2SO4 bath to remove any traces of oxidizable matter, then sonicated for 2 min in deionized water. Final cleaning to eliminate any contaminants (e.g., a surface oxide layer) that might interfere with the electrochemical measurements was carried out at the start of each experiment by cycling the potential up to 16 times over the working range (typically −500 to +200 mV vs AgCl/Ag) at 20 mV s−1 until the cyclic voltammogram (CV) showed a constant limiting current Ilim. These measurements of Ilim gave values of the diffusion coefficient D of Ru(NH3)63+

D = Ilim/4FrC

(1)

(where C is the concentration of Ru(NH3)63+, F is the Faraday constant, and r is the radius of the UME disk) in reasonable agreement with those in the literature; as noted below, however, Ilim measured from a CV depends on the identity and concentration of the supporting electrolyte and comparisons can only be made where these are the same. For example, for UMEs made from Au or Pt wire of diameter 2r = 25.0 μm (according to the wire manufacturer), Ilim for 5.0 mmol L−1 [Ru(NH3)6]Cl3 in 0.1 mol L−1 KCl at 25 °C was 23−24 nA, corresponding to D = 9.5 × 10−6 cm2 s−1; literature values of D for Ru(NH3)63+ for these conditions range from 6.4 × 10−6 cm2 s−1 to 9.4 × 10−6 cm2 s−1.19,49−52 These observations, together with the consistency of the kinetic results between different experiments as described below, indicate that the potential cycling procedure did not have adverse effects on the electrochemical measurements. Materials. Deionized water was further purified to ≥18.0 MΩ cm by passage through a Barnstead E-Pure train. [Ru(NH3)6]Cl3 (Strem Chemicals, 99%), triflic acid (Sigma Aldrich, 98%), hydrochloric acid (Merck), perchloric acid (Baker), NaCl (Fisher Certified) and KCl (Fisher Certified) were used as received, and KCF3SO3 was either prepared as previously described53 or purchased from Alfa Aesar and recrystallized from methanol. [Ru(NH3)6](CF3SO3)3 was prepared from aqueous [Ru(NH3)6]Cl3 by removal of Cl− with AgCF3SO3, followed by precipitation and recrystallization of [Ru(NH3)6](CF3SO3)3 from aqueous CF3SO3H, as described by Lavallee et al.;54 the purity of the colorless needles was established by multiple CHN microanalyses (calc.: C, 5.54; H, 2.79; N, 12.92; found: C, 5.67; H, 2.84; N, 12.86%) and by the molar absorbance of aqueous solutions (460 ± 10 L mol−1 cm−1 at 275 nm54). Electrochemical Measurements. CV and variable-frequency ac impedance measurements were made with either a thermostatted conventional three-electrode cell or the high-pressure three-electrode Teflon cell previously described,53 using a Model CHI650C electrochemical workstation with a Model CHI200 picoamp booster and Faraday cage (CH Instruments, Austin, TX); backup measurements using a Model CHI650B workstation gave identical results. The reference electrode was Ag/AgCl/KCl (satd. aq. at 25 °C, or, for experiments at variable P or T, 4.0 mol L−1, i.e., just below saturation55), freshly prepared before each day’s series of measurements by anodic electrolysis of a silver wire in 4.0 mol L−1 KCl solution at 0.7 V vs Ag/AgCl/KCl(satd) for 20 min. The working electrode was a Pt or Au UME, and the counter electrode a Pt wire 2758


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(typically ⌀ 0.5 mm, ∼1 cm long). Experiments at ambient pressure were conducted with the cell either in the CHI Faraday cage or completely enclosed in grounded Al foil, whereas for the high pressure experiments it was sufficient simply to ground the pressure vessel; in all cases, the external connectors were sheathed in grounded Al foil. The pressure vessel and pressure train have been described elsewhere;53 the pressure transmitting fluid was mixed hexanes, separated from the hydraulic oil of the manual pump and intensifier by a vessel with a free piston. All variable-pressure experiments were run at 25.0 ± 0.1 °C, which was maintained with externally thermostatted water circulating through the pressure vessel jacket and measured inside the pressure vessel before and after the pressure cycle. For experiments at variable temperature and 0.1 MPa, a glass cell incorporating a jacket for circulating water from the external thermostat was used, and temperatures within the sample were measured (±0.1 °C) with a calibrated thermistor encased in an inert plastic. All solutions contained 5.0 mmol L−1 [Ru(NH3)6]Cl3 or [Ru(NH3)6](CF3SO3)3 and were purged with Ar for 30 min before the experiments. For measurements at ambient pressure, an Ar atmosphere was maintained. Spectrophometric measurements at 275 nm showed that [Ru(NH3)6](CF3SO3)3 solutions underwent no significant decomposition at near-ambient temperatures over at least 24 h. Measurements of the cell impedance were made using the supplied CHI software by applying an ac signal of amplitude 10 mV and frequency f within the range 0.96−96 kHz (depending on reaction rate being measured) superimposed on a dc signal that was swept typically over 250−350 mV on each side of the formal potential of the Ru(NH3)63+/2+ couple (∼ −130 mV vs Ag/AgCl/KCl(satd)). Scan rates were normally 10 mV s−1.

where Rct is the charge transfer resistance.22,23,58 Extrapolation of Zf′ to infinite frequency gives Rct, from which the standard rate constant kel for the electrode reaction can be calculated from eq 3, in which n is the number of electrons transferred per mol (here, n = 1), a is the area of the UME disk, C is the bulk concentration of the electroactive species, and the other symbols have their usual meaning in the SI. kel = RT /n2F 2aCR ct

If a UME is performing correctly, the CV should be a tight sigmoidal trace rather than the “duck” shape familiar from measurements with conventional electrodes. This was checked as a prelude to each impedance measurement, as exemplified for a series of supporting-electrolyte concentrations by Figure 2 in which it may be seen that the ideal sigmoidal shape is more closely approached the higher the concentration of supporting electrolyte (i.e., the faster the electrode reaction, see below). Values of the transfer coefficient α were calculated from eq 5, in which Emax is the potential of maximum real admittance Y′ (cf. Figure 3) and E1/2 is the CV half-wave potential; in all cases, |Emax − E1/2| ≤ 5 mV, whence α = 0.50 ± 0.05 (cf. Muzikár ̌ and Fawcett22). For example, for [Ru(NH3)6]Cl3 reduction on a 25 μm Au UME in 0.1 mol L−1 KCl at 25 °C, Emax = −0.134 V and E1/2 = −0.135 V, giving α = 0.51. Emax = E1/2 + (RT /F ) ln[α /(1 − α)]

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Figure 1. Simplified equivalent circuit for an electrochemical cell with UME working electrode.

impedance of an electrochemical cell to the faradaic impedance Zf, the Warburg (diffusional) impedance ZW, the uncompensated solution resistance Ru, and the double-layer capacitance Cdl. The Warburg impedance can be neglected at the ac frequencies used in our experiments.58 Before making an impedance measurement, the uncompensated resistance Ru was measured and automatic correction for it was implemented using the CHI software. The impedance Zf can be resolved using the CHI software into real (Zf′) and imaginary (Zf″) components, each of which should be a linear function of ω−1/2, where ω = 2πf, with slope s for a simple electron transfer process: (2)

Zf ″ = sω−1/2

(3)

(5)

If the CV was satisfactory, impedance measurements were then made as a function of the dc potential at selected frequencies. The frequencies typed in differed slightly from the work-station’s actual operating frequencies f, which were recorded and converted to angular frequencies ω = 2πf. Whereas the uncompensated resistance can be corrected for by direct subtraction from the real impedance, correction for the double-layer capacitance Cdl requires conversion to admittances Yf (reciprocals of Zf). Typical real and imaginary admittances Yf′ and Yf″ are plotted in Figure 3, which also illustrates the importance of correcting for Ru, at least in Yf″. The absence of substantial distortions and baseline noise in admittance vs potential plots such as Figure 3 indicated that instrumental and other artifacts that may occur at high frequencies59 were negligible. In accordance with eqs 2 and 3, Zf′ and Zf″ for a given experiment were plotted together against ω−1/2 (a Randles plot),58 as shown in Figure 4 for an experiment with 12 data points spanning a wide frequency range (0.962−46.3 kHz). A result was accepted only if, within the experimental uncertainty, the Zf′ and Zf″ plots were linear, their slopes s were the same, and Zf″ extrapolated to zero at infinite frequency (ω−1/2 = 0), confirming the absence of instrumental distortions at high frequencies. The intercept of the Zf′ plot then gave Rct, from which the rate constant kel could be calculated from eq 4; in practice, however, errors in the impedances Zf′ and Zf″ tended to be similar, and averaged values of (Zf′ − Zf″) were therefore used in place of Rct, giving a modest improvement in the standard error. For example, least-squares regression of the Zf″ data of Figure 4 gave a slope s of 6.87 ± 0.09 MΩ rad1/2 s−1/2 and intercept −0.57 ± 0.54 kΩ (r2 = 0.9982); thus, the intercept is negligible on the impedance scale, as eq 3 requires, and the lower straight line in Figure 4 is therefore plotted with the intercept set to zero. For Zf′, regression gave a slope s = 7.01 ± 0.13 MΩ rad1/2 s−1/2, which is not statistically distinguishable from that for Zf″, as required by eqs 2 and 3,

RESULTS In the following, the usual assumption56 is made that the diffusion coefficients of Ru(NH3)63+ and Ru(NH3)62+ are close enough to be taken as approximately the same, as literature data affirm.16,21,57 Electrode and Electrolyte Effects. Figure 1 shows a simplified equivalent (Randles) circuit relating the overall

Zf ′ = R ct + sω−1/2

(4)

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Figure 2. Cyclic voltammograms of the reduction of 5.0 mmol L−1 [Ru(NH3)6](CF3SO3)3 at a Pt disk (⌀ 10 μm) at 25.0 °C; scan rate = 10 mV s−1. Concentration of KCF3SO3 supporting electrolyte (mol L−1) = 0 (black), 0.05 (red), 0.10 (green), 0.15 (blue), and 0.20 (gray).

Figure 3. Real (Y′) and imaginary (Y″) admittances as a function of potential vs Ag/AgCl for reduction of [Ru(NH3)6]Cl3 (5.0 mmol L−1) at a Pt disk (⌀ 25 μm) in 0.1 mol L−1 KCl at 30 °C and f = 3205 Hz. Blue, Yf′ uncorrected for uncompensated resistance Ru; black, corrected Yf′; green, uncorrected Yf″; red, corrected Yf″. Scan rate 10 mV s−1.

and an intercept Rct = 17.9 ± 0.8 kΩ (r2 = 0.9966), cf. an average (Zf′ − Zf″) of 19.1 ± 0.4 kΩ which was used to calculate kel. In practice, good Randles plots and acceptable values of kel could usually be obtained with as few as 4−5 choices of f. Again, the consistency of the data at the highest frequencies with the rest of the plot affirmed correct instrumental function.59 Table 1 lists standard electrode reaction rate constants kel derived from Randles plots in which the Zf′ and Zf″ lines were parallel, the Zf″ plot extrapolated to zero at ω−1/2 = 0, and the data scatter was acceptable, all within the experimental uncertainty. The calculation of kel from eq 4 required values of the effective areas a of the microelectrode disks; these could

be determined either approximately from the manufacturer’s wire diameters or more precisely from the limiting currents Ilim of CVs of either Ru(NH3)63+ or Fe(CN)63− solutions:

a = π (Ilim/4nFDC)2

(6)

Ru(NH3)63+19,22,49−52

where D is the diffusion coefficient of or Fe(CN)63− (7.63 × 10−6 cm2 s−1).60 Values of a from eq 6 were slightly greater than calculated from the geometrical crosssection of the wire (e.g., in a typical experiment with Au and Pt UMEs made from wire of diameter 25.0 μm, the areas measured according to eq 6 corresponded to ⌀ 26.0 and 29.7 μm, respectively); these discrepancies are attributable to microscopic roughness of the UME surfaces.61 For the 2760


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Pressure Effects. The results reported in this section all refer to reductions of Ru(NH3)63+ at UMEs of diameter 25.0 μm, as UMEs of smaller diameters proved to be too fragile to give reproducible measurements at variable pressure. Figure 6 shows the pressure dependences of the half-wave potential (E1/2, from the midpoints of CVs run before each set of impedance measurements at a given pressure P) and of the corresponding standard rate constant kel for a typical [Ru(NH3 ) 6](CF 3SO3 )3 electrode reaction, in this case reduction at a gold UME in 0.10 mol L−1 KCF3SO3 at 25.0 °C. Both plots are linear within experimental uncertainties. It was important to show that the measurements taken with increasing pressure (filled symbols) were consistent with those subsequently taken with decreasing pressure (hollow symbols)that is, that no time-dependent changes such as decomposition of the Ru complexes occurred over the several hours’ duration of the experiment.62 For the lower plot in Figure 6, E1/2 = (−0.196 ± 0.002) − (2.49 ± 0.16) × 10−4P, from which the volume of reaction ΔVel = −F(∂E1/2/∂P)T cm3 mol−1 for the Ru(NH3)63+ reduction half-cell relative to Ag/ AgCl is 24.0 ± 1.6 cm3. The UME-CV method, however, is not well suited to precise measurements of the small changes in E1/2, and ΔVel values obtained in this way ranged from 20.3 ± 1.6 cm3 mol−1 for reduction of [Ru(NH3)6](CF3SO3)3 in 0.10 mol L−1 KCF3SO3 at a Pt UME to about 25 cm3 mol−1 for [Ru(NH3)6]Cl3 in 0.1 mol L−1 KCl at Au and Pt UMEs. These results are nevertheless consistent with the definitive ΔVel measurements of Tregloan and co-workers63−65 for reduction of Ru(NH3)63+ made at conventional electrodes (20.2 ± 0.4 cm3 mol−1 in 0.1 mol L−1 KNO3 at Au, and 19.7 ± 0.6 cm3 mol−1 in 0.1 mol L−1 NaClO4 at Hg/Au, relative to Ag/AgCl). The pressure dependence of ln kel was linear, within the experimental uncertainty, in all cases studied; in other words, the volume of activation ΔVel⧧ was effectively constant over the 200 MPa pressure range. For [Ru(NH3)6](CF3SO3)3 in 0.10 mol L−1 KCF3SO3 at a gold UME (upper frame of Figure 6), ln kel = (−1.999 ± 0.030) + (6.15 ± 0.30) × 10−3P for P in MPa, whence ΔVel⧧ = −15.3 ± 0.7 cm3 mol−1 for 0.10 mol L−1 KCF3SO3 at Au; for the same system at a Pt UME, ΔVel⧧ = −15.9 ± 1.1 cm3 mol−1. For reduction of [Ru(NH3)6]Cl3 (5.0 mmol L−1) in 0.10 mol L−1 KCl, ΔVel⧧ = −12.3 ± 1.0 and −12.3 ± 0.6 cm3 mol−1 at 25 μm Au and Pt UMEs, respectively. Thus, ΔVel⧧ is independent of the UME metal but shows some significant dependence on the nature of the anion of the supporting electrolyte. Measurements of ΔVel⧧ for perchlorate media at variable pressure were impractical, as the rate constants, already fast at ambient pressure, would become too fast for accurate measurement at increased pressures. The possibility of oxidation of the Ru complexes by ClO4− over the time-scale of a pressure cycle was also a concern.

Figure 4. Randles plot for the reduction of [Ru(NH3)6](CF3SO3)3 (5.0 mmol L−1) in aqueous KCF3SO3 (0.20 mol L−1) at a gold disk electrode (⌀ 25 μm) at 25.0 °C. Red data: real impedance Zf′. Green data: imaginary impedance Zf″. Average uncompensated resistance was 7.59 ± 0.08 kΩ.

purposes of this study, however, relative rather than absolute values of kel are required in assessing electrolyte, pressure, and temperature effects, and geometrical values of a based on the wire diameters given by the manufacturers were used in calculating the kel data of Table 1, which is common practice in UME studies; possible contamination of the UMEs in measuring Ilim prior to an experiment was thereby avoided. The uncertainties cited in Table 1 represent the goodness of fit to eqs 1 and 2 rather than absolute accuracy of kel; nevertheless, reasonable agreement may be noted between kel values obtained for given conditions but with different personnel and sources of chemicals and materials. Agreement with literature values of k el, 13,15−23 where conditions were comparable, was also satisfactory, given the difficulties in obtaining reproducible kel for fast electrode reactions and the lack of clarity in some earlier publications (e.g., Iwasita et al.15,16) as to whether appropriate corrections (e.g., for uncompensated resistance, important for rapid electrochemical reactions such as Ru(NH3)63+/2+50) had been applied. Table 1 shows that the main influences on kel are supporting electrolyte identity and concentration, and the UME diameter; the identity of the polycrystalline UME metal (Pt vs Au) has little effect. Temperature Dependence of kel. The temperature dependence of kel for [Ru(NH3)6](CF3SO3)3 in 0.1 mol L−1 KCF3SO3 at a Pt UME is shown in Figure 5 as an Arrhenius plot (ln kel = ln A − Ea/RT) for which the activation energy Ea = 18.8 ± 1.1 kJ mol−1 and A = 4.3 × 102 cm s−1. Thus, the temperature sensitivity of kel is quite low. Use of Eyring enthalpies ΔHel⧧ (= Ea − RT) and entropies ΔSel⧧ of activation was avoided, as ΔSel⧧ values as normally calculated depend on ̈ comparison with other the units of the rate constants, and naive entropy parameters could be misleading. For the reduction of [Ru(NH3)6]Cl3 in 0.1 mol L−1 KCl at a gold UME (⌀ 25 μm), 5.3−29.1 °C, Ea was found to be 24.8 ± 1.3 kJ mol−1 (Supporting Information, Figure S1).

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DISCUSSION Cyclic Voltammetry. The maxima |Ilim| of the (negative) CV currents for reduction of Ru(NH3)63+ were markedly dependent on the concentrations of the supporting electrolyte, as shown for example in Figure 2. This reflects a substantial contribution from the migration current,66 which is negative for the reduction of a cation at an electrode but tends to zero as the concentration of the supporting electrolyte (and hence the solution conductivity) is increased. Thus, as shown in Figure 2, the observed |Ilim| for the reduction of [Ru(NH3)6](CF3SO3)3 was largest when no supporting electrolyte was present, but 2761


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Table 1. Dependence of Standard Rate Constants kel for the Reduction of Aqueous Ru(NH3)63+ at Polycrystalline Au and Pt UMEs on UME Disk Diameter and Supporting Electrolyte Concentrationa X in [Ru(NH3)6]X3 Cl

electrolyte, mol L−1

Pt 25 μm

0.089 ± 0.001

KCl, 0.05

0.234 ± 0.005

0.08 0.10

CF3SO3

Au 25 μm

none

0.54 ± 0.01 0.62 ± 0.03c

0.52 ± 0.01 0.43 ± 0.01c 0.49 ± 0.03b,c

Au 12.7 μm

0.66 0.71 1.78 2.20

± ± ± ±

Pt 10 μm

0.01 0.01b 0.03 0.05

0.15 0.20

0.88 ± 0.03 1.05 ± 0.01

HCl, 0.02 0.05 0.10

0.063 ± 0.001 0.29 ± 0.01 0.62 ± 0.01

0.26 ± 0.01 0.65 ± 0.01 1.84 ± 0.13

NaCl, 0.10

0.66 ± 0.01

1.86 ± 0.06

KO3SCF3, 0.10

0.28 ± 0.01

HClO4, 0.02 0.05

0.21 ± 0.01 0.84 ± 0.01

none

0.088 ± 0.001

KO3SCF3, 0.05 0.10 0.15 0.20

0.21 ± 0.01 0.39 ± 0.01

0.18 ± 0.01 0.38 ± 0.01

0.21 ± 0.01 0.46 ± 0.01

0.57 ± 0.01

0.53 ± 0.01

0.85 ± 0.02

HClO4, 0.02 0.05

0.95 ± 0.03

1.16 ± 0.17b

0.38 ± 0.01 0.29 ± 0.02b,c

0.98 ± 0.02b,c

0.27 ± 0.01

0.21 ± 0.01 0.68 ± 0.01 0.97 ± 0.01 1.16 ± 0.01

0.33 ± 0.01

a 25.0 °C, 0.1 MPa; [Ru(NH3)63+] = 5.0 mmol L−1. Uncertainties reflect standard errors in Rct or average (Zf′ − Zf″). bMeasurements by G.L.; all others by V.V. cExtrapolated to 0.1 MPa from high pressure kinetic measurements.

ideal tight sigmoid more closely in presence of ≥0.1 mol L−1 supporting electrolyte, which also gave higher rate constants (Table 1) and generally better fits to eqs 2 and 3. Measurements of kel at variable temperature and pressure were therefore conducted using 0.1 mol L−1 KCl or KCF3SO3 as supporting electrolyte. Factors Affecting the Rate Constants. The following observations emerge from Table 1. (1) Although one special advantage of UMEs is that they can yield kinetic data in absence of a supporting electrolyte, values of kel for [Ru(NH3)6]X3 without an added electrolyte are presented only for X = Cl and CF3SO3 at a 25 μm gold UME; for measurements on other systems without a supporting electrolyte, the data quality criteria given above were not met. (2) For a given anion X, kel is about the same at polycrystalline Au and Pt UMEs of the same diameter compare, for example, data for 0.10 mol L−1 added KCl, or for 0.10 mol L−1 KCF3SO3, at 25 μm UMEs. Muzikár ̌ and Fawcett23 found that, for reduction of Ru(NH3)63+ at singlecrystal Au UMEs, kel at Au(111) was significantly larger than at Au(100), which may account in part for the difficulty in obtaining reproducible kel values between polycrystalline UMEs but also diminishes the effectiveness of an apparent lack of dependence of kel on the identity of the metal of the electrode

Figure 5. Temperature dependence of kel for reduction of [Ru(NH3)6](CF3SO3)3 in aqueous 0.1 mol L−1 KCF3SO3 at a Pt UME (⌀ 25 μm).

decreased with increasing concentrations of added KCF3SO3 (cf. the reduction of Tl(aq)+ at a mercury-on-silver UME in aq. LiClO467). Moreover, the shape of the CVs approached the 2762


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Mirkin gives kel = 2.6 cm s−1). For our purposes of determining electrolyte, pressure, and temperature effects, however, comparison of apparent values of kel at disk UMEs of a common diameter was sufficient. (4) The strong accelerating effect of supporting electrolytes on kel is a function of the electrolyte concentration but is due specifically to the anion. Thus, for supporting electrolytes MX at 0.1 mol L−1, kel was essentially the same for M = K, Na, and H when X was Cl. For different X, however, kel increased in the sequence CF3SO3 < Cl ≪ ClO4. For reduction of [Ru(NH3)6]Cl3 at a gold electrode (⌀ 25 μm) at 25.0 °C (the most extensive data set), kel was a linear function of [Cl−] (Supporting Information, Figure S2), and a least-squares regression of the data of Table 1 gave kel/cm s−1 = (−0.02 ± 0.05) + (5.11 ± 0.34)[Cl−]total, where [Cl−]total includes Cl− from both KCl (if present) and [Ru(NH3)6]Cl3; the fact that the intercept is zero within the error limit implies that the reduction reaction rate would be negligibly small in the hypothetical case in which no chloride was present. Thus, for the system with chloride as the only anion present, the electrode reaction mechanism intimately involves the anion, even in absence of the supporting electrolyte. The limited data for the triflate-only system at 25 and 10 μm disks are better represented by curves passing through the origin; for the 10 μm Pt disk, an empirical quadratic fit with R2 = 0.9994 extrapolated to hypothetical zero triflate with kel0 = 0.050 ± 0.020 cm s−1 (Supporting Information, Figure S3), from which case it can again be inferred that the Ru(NH3)63+/2+ electrode reaction rate would be very small in the hypothetical absence of the anion. (5) Instrumental limitations set the upper limit of kel obtainable at about 2 cm s−1, and accordingly no data for [MX] > 0.20 mol L−1 are listed in Table 1. For the same reason, kel values for reduction of [Ru(NH3)6]X3 (X = Cl or CF3SO3) in HClO4 are listed only for [ClO4−] up to 0.05 mol L−1, beyond which the reaction rates were too high to measure with the desired accuracy. The standard rate constants at a gold UME of diameter 12.7 μm in 0.02 mol L−1 HClO4 are somewhat lower than that reported by Muzikár ̌ and Fawcett22 (0.54 cm s−1) for the same system (X presumably was Cl) at a polycrystalline gold UME of diameter 12.5 μm (6.25 μm radiusapparently misprinted as diameter in Table 2 of ref 22). The direct proportionality of kel for the Ru(NH3)63+/2+ cation−cation electron transfer reaction at Au or Pt UMEs in all-chloride systems to the total anion (chloride) concentration, independently of the accompanying alkali-metal or H cations, recalls (reversed charge-type notwithstanding) that of both kel and the corresponding homogeneous self-exchange rate constant kex for the AlW12O405−/6− anion−anion electron transfer reaction on the cation (various alkali metal ions) concentration, independently of the accompanying anions.53 For AlW12O405−/6−, it was shown53 that the variable relevant to the cation-specific catalysis was simply the concentration of the cation, and not Debye−Hückel, Gouy−Chapman, ion-pairing, or other medium effects. Specific alkali-metal ion catalysis of other anion−anion electrode and self-exchange reactions such as PW 12 O 40 3−/4− , CoW 12 O 40 5−/6− , Mo(CN) 8 3−/4− , W(CN)83−/4−, and Os(CN)63−/4− has also been described,70−72 while for the Fe(CN)63−/4− homogeneous self-exchange reaction alkali-metal cation catalyzed pathways are completely dominant unless the alkali-metal cations are sequestered with crypt-2.2.2 or 18-crown-6 to expose the very slow direct exchange of Fe(CN)63− with Fe(CN)64−.62 Measurement of kex

Figure 6. Pressure dependences of the half-wave potential E1/2 relative to Ag/AgCl (lower frame), and the standard rate constant kel (upper frame), for reduction of [Ru(NH3)6](CF3SO3)3 (5.0 mmol L−1) in 0.10 mol L−1 KCF3SO3 at a gold UME (⌀ 25 μm) at 25.0 °C; pH ≈ 5. Filled symbols: increasing pressure. Open symbols: decreasing pressure.

as a criterion of adiabaticity. With this reservation, and noting the argument of Gosavi and Marcus10 discussed in the Introduction, the reduction of Ru(NH3)63+ at Au and Pt UMEs can be taken to be either essentially adiabatic or at least not strongly nonadiabaticour data do not distinguish definitively between these two possibilities. In any event, the practical issue is that the metal of the electrode (Au vs Pt) has no bearing on the interpretation of the measurements reported here. (3) The apparent values of kel increase substantially on going from an electrode diameter of 25 μm to 12.7 and then to 10 μm. Although the upper limit of disk diameter for true UME behavior, with convergent radial diffusion of the electroactive species to the disk, is usually taken to be ∼50 μm (i.e., radius 25 μm),61 it is possible that a contribution from planar diffusion of Ru(NH3)63+ may have persisted in the disks of larger diameter, resulting in the observation of reaction rates slower than the “true” value. The slightly broadened shapes of some of the CVs in Figure 2 are consistent with this interpretation.68 Indeed, Sun and Mirkin69 found that the reduction of [Ru(NH3)6]Cl3 in 0.5 mol L−1 KCl at Pt nanoelectrodes of radii 282−14.7 nm gave kel values that increased from ∼14 to ∼19 cm s−1 over that range of radii (mean kel = 17.0 ± 0.9 cm s−1), so that it would appear that the electrode disk radius effect continues below the UME size range (extrapolation of our data for a Pt UME of diameter 25 μm to the KCl concentration used by Sun and 2763


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kel vs [Cl−] plot of Supporting Information, Figure S2, while still less surface would be blocked by the very weakly adsorbed ClO4− (in our experiments with perchlorate media, however, either Cl− or CF3SO3− was also present to the extent of 15.0 mmol L−1). For CF3SO3−, an approach to saturated blocking at high [triflate] even at the Ru(NH3)63+/2+ formal potential of +0.07 V vs NHE could give the curve of Supporting Information, Figure S3. Thus, anions could affect the Ru(NH3)63+/2+ exchange rate in two opposing ways retardation through partial electrode surface blockage (more so with triflate), and acceleration through an essential involvement in the Ru(NH3)63+/2+ electron transfer process (particularly with chloride, which may interact in a specific way with the Ru complexes). Temperature Effects on the Electrode Reaction Rate. The primary purpose in estimating the temperature dependences of kel in various environments was the empirical one of assessing the relevance of measurements at 25 °C to the broader near-ambient range. The observed Arrhenius activation energies Ea are small, as expected in view of the very small change in Ru−N bond lengths on going from Ru(NH3)63+ to Ru(NH3)62+ (+4.0 ± 0.4 pm91) with a correspondingly small Marcus internal reorganization energy (4 ± 2 kJ mol−192 for the homogeneous electron transfer reaction and hence 2 ± 1 kJ mol−1 for the electrode reaction1). Values of Ea ranged from 19 kJ mol−1 for the triflate salt in 0.1 mol L−1 KCF3SO3 at a Pt UME to 25 kJ mol−1 for [Ru(NH3)6]Cl3 in 0.1 mol L−1 KCl at a gold UME. These activation energies cannot, however, be simply interpreted in terms of electron transfer dynamics unless it can be shown that the double layer does not change with temperature. This will not be the case if the analysis of the preceding paragraph is applicable, since, as noted above, literature values of ΔHads0 are substantially negative for both CF3SO3− and Cl−, meaning that the degree of anion adsorption would be reduced as the temperature is increased. As only a minor fraction of the electrode surface would be blocked by either CF3SO3− or Cl− at the formal potential of the Ru(NH3)63+/2+ couple, the correction of Ea for this effect, if real, would not be large. Pressure Effects on the Electrode Reaction Rate. It is possible to predict a value of ΔVel⧧ for a simple electrode reaction from the analogous parameter ΔVex⧧ for the corresponding homogeneous self-exchange reaction using the relation

for the Ru(NH3)63+/2+ self-exchange73−75 is technically challenging (kex = 3.2 × 103 L mol−1 s−1 at 25 °C in 0.1 mol L−1 CF3SO3H74), but a linear dependence of kex for that reaction on chloride concentration has been reported, although a definitive separation of a specific Cl− catalysis from ionic strength effects could not be made.75 In this connection, we note that, for the homogeneous Ru(en)33+/2+ self-exchange reaction (en = 1,2-diaminoethane), kex is some 20-fold higher in chloride than in comparable triflate media,76 so that the Cl− catalysis effect found in this study may reflect a specific affinity of Cl− for Ru am(m)ine complexes. To summarize, the dominant counterion (Cl− and CF3SO3−) catalysis of the Ru(NH3)63+/2+ electrode reaction reported here, and possibly also Cl− catalysis of the homogeneous Ru(NH3)63+/2+ selfexchange,75 have precedents in the counterion catalysis of the electrode and homogeneous self-exchange electron transfer kinetics of several anion−anion couples. In interpreting the role of CF3SO3−, Cl−, and ClO4− in promoting the Ru(NH3)63+/2+ electrode reaction, the tendency of these anions to adsorb on the Au and Pt electrode surfaces should be considered. For the Cl−-catalyzed electrode reaction, the direct proportionality of kel to [Cl−] suggests that any such adsorption is far from saturation over the concentration ranges used in our experiments, whatever the kinetic role of Cl− might be. The specific adsorption of Cl− on Pt77−82 and Au81,83−85 is known to be well advanced at potentials on the order of +0.8 V vs NHE, but only incipient at the formal potential of the Ru(NH3)63+/2+ electrode reaction (∼ −0.13 V vs Ag/AgCl(satd. KCl), ∼ +0.07 V vs NHE; the potential sweeps in our impedance measurements, however, extended 250−350 mV on either side of this). The adsorption of ClO4− on Pt or Au in this potential range is generally considered negligible (most of the Cl− adsorption studies cited here involved background perchlorate), although specific adsorption of perchlorate does occur at high potentials (>1 V).86,87 For our study, CF3SO3− was chosen as an alternative to perchlorate for reasons given in the Introduction, on the assumption that triflate would behave similarly to perchlorate with respect to adsorption on Au and Pt electrode surfaces. Indeed, Lipkowski, Burgess, and co-workers have reported88 that CF3SO3− adsorbs only very weakly at a positively charged Au electrode surface, and experimental data supplied privately by Lipkowski and Burgess confirm this (although coadsorption of CF3SO3− with a cationic surfactant on Au was noted89). Bockris et al.,90 however, found that adsorption of aqueous CF3SO3− was extensive on a Pt electrode at 0.8 V vs NHE (ΔHads0 = −44 kJ mol−1 and ΔSads0 = −97 J K−1 mol−1; cf. −30 kJ mol−1 and −80 J K−1 mol−1, respectively, for Cl− on Pt82), and was substantial even at −0.05 V, with the consequence that an adsorption-free reference potential could not be reached before H2 evolution set in. It is possible that adsorption of triflate is important on Pt but not on Au. However, since the data of Table 1 show that kel for the Ru(NH3)63+/2+ electrode reaction at both Au and Pt increased in the sequence CF3SO3− < Cl− < ClO4−, it may be conjectured that partial blockage of the electrode surface by specific adsorption of these ions occurred and decreased in this order if the results of Bockris et al.90 are applicable at the formal potential of the Ru(NH3)63+/2+ couple on Au and Pt UMEs, then the bulky triflate ion could be particularly effective in blocking a substantial fraction of the electrode surface. The anion-free surface would then carry the anion-modulated electron transfer reaction. Only a small fraction of the electrode surface would be blocked by chemisorbed Cl−, giving the linear

ΔVel ⧧ ≈

1 ΔVex ⧧ 2

(7) 1

derived from Marcus theory, but the numerous reported experimental difficulties73−75 effectively precluded a direct determination of ΔVex⧧ for the Ru(NH3)63+/2+ self-exchange reaction in homogeneous solution. A procedure described elsewhere1 that works well for simple electron transfers in aqueous solutions allows the calculation of a theoretical ΔVex⧧ for a homogeneous self-exchange reaction ΔVex ⧧(theor) = ΔVIS⧧ + ΔVOS⧧ + ΔVCOUL ⧧ + ΔVDH ⧧ (8)

where IS, OS, COUL, and DH refer respectively to the contributions of the pressure-dependences of the inner-sphere reorganization, outer-sphere (solvational) reorganization, Coulombic work terms, and activity coefficient (Debye−Hückel) corrections. For Ru(NH3)63+/2+, ΔVIS⧧ will be negligible (the corresponding reorganization energy is only 4 ± 2 kJ mol−192). 2764


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declines by 27% from 0 to 200 MPa at 25 °C. This decline would reduce any catalysis due to ion pairing, leading to less negative values of ΔVex⧧ and ΔVel⧧ than otherwise expected. The same factors that favor breakup of ion pairs by increasing pressure will also promote desorption of anions from electrode surfaces. For example, molecular dynamics calculations95 show that chloride ion is “contact adsorbed” on a Pt electrode and solvated locally by adsorbed water, which implies that Cl−(aq) is partially desolvated on adsorption and also displaces some existing adsorbed waterboth of which processes will be disfavored by increasing pressure. Consequently, if, as suggested above, the catalytic efficacy sequence CF3SO3− < Cl− ≪ ClO4− reflects in part decreasing electrode surface blockage, increasing pressure will be particularly effective in accelerating the Ru(NH3)63+/2+ electrode reaction for CF3SO3− as the anion (most negative ΔVel⧧, −16 cm3 mol−1), less so for Cl− (ΔVel⧧ = −12 cm3 mol−1), and least for ClO4− which is presumably not specifically adsorbed (ΔV el ⧧ was not measurable for ClO4−). Against this interpretation are the uncertainty in the article by Bockris et al.90 regarding the extent of adsorption of CF3SO3− on Pt at potentials near 0.0 V vs NHE, and the report by Lipkowski et al.88 that adsorption on Au is negligible at such potentials; this topic deserves to be revisited. In any event, since the anions are evidently intimately involved in the electron transfer process itself, the predictions of the simple Marcus-based theory (eqs 6−11) are not applicable to ΔVel⧧. An alternative interpretation of the unexpectedly strongly negative ΔVel⧧ for Ru(NH3)63+/2+ electrode reaction notes that, for the comparable RuN6 couple Ru(en)33+/2+, the measured ΔVel⧧ and ΔVex⧧ are also more negative than expected from theory, being respectively −7.5 ± 0.3 (at glassy C in 0.4 mol L−1 KCl or CF3COONa) and −15.1 ± 1.7 cm3 mol−1 (from the Marcus cross-relationencouragingly, ΔVel⧧ = 0.5ΔVex⧧ as predicted),76 suggesting that the departure from theoretical expectations has origins peculiar to Ru am(m)ine chemistry; the fact that ΔVel⧧ is more negative for the Ru(NH3)63+/2+ couple than for Ru(en)33+/2+ may reflect the cation size difference (eqs 6−11).1 Since the free energy barrier for RuIII/II electron transfer is almost entirely due to solvent reorganization, it may be inferred that a strong increase in specific solvation, over and above the Born-continuum solvent effects invoked in basic Marcus theory, occurs in electron transfer in RuIII/II am(m)ine couples and makes strongly negative contributions to ΔVel⧧ and ΔVex⧧. Indeed, specific interactions between Ru(NH3)63+ and the surrounding water molecules in aqueous solution are evident in 1H2O and H217O NMR spectra,96 and theoretical calculations indicate that electron transfer to polar solvents such as water affects the metal-toligand charge transfer bands of ruthenium(II) ammines.97 Strong solvent dependences of the optical spectra of complexes containing the Ru(NH3)53+ group confirm that H-bonding of the ammine protons to polar solvent molecules is extensive, probably resulting in mixing of solvent character into the dπ orbitals of Ru.98−100 The intervalence electron transfer band due to weakly coupled RuII and RuIII in (NH3)5RuII(μL)RuIII(NH3)55+ (L = 2,6-dithiaspiro[3.3]heptane) in D2O exhibits a large red shift with rising pressure, rather than the expected blue shift, and this is attributable to pressureenhanced hydrogen bonding of the ammine ligands to the solvent.101 In electron transfer between Ru ammines and cytochrome c, either in Ru-modified cyt c or between Ru(NH3)5(ligand)3+/2+ and cyt cII/III, the volume changes are

If r1 and r2 are the radii of Ru(NH3)63+ and Ru(NH3)62+, respectively, z1 and z2 are the charge numbers, σ is the separation between these ions at the moment of electron transfer (presumed = r1 + r2), ε and n are the relative permittivity (dielectric constant) and refractive index of the solvent, A and B are the Debye−Hückel parameters at atmospheric pressure, å is the DH contact distance (effectively r1 plus the anion radius), I is the ionic strength, and β is the isothermal compressibility of the solvent, then ΔVOS⧧ = (NAe 2 /16πε0)[(2r1)−1 + (2r2)−1 − σ −1] [∂(n−2 − ε−1)/∂P]T

(9)

ΔVCOUL ⧧ = [NAz1z 2e 2 /4πε0σ ](∂ε−1/∂P)T

(10)

ΔVDH ⧧ = [RTz1z 2AI1/2/(1 + BåI1/2)2 ][(∂ln ε /∂P)T (3 + 2BåI1/2) − β ]

(11) 3+

Ru(NH3)62+,

−

If the effective radii of Ru(NH3)6 , Cl , and CF3SO3− are taken to be 340, 344, 181, and 340 pm, respectively, then, for 25 °C and I = 0.12 mol L−1 as in our variable-pressure experiments and the midrange pressure of 100 MPa, ΔVOS⧧ (−8.9 cm3 mol−1) is seen to be dominant because ΔVDH⧧ (+2.7 cm3 mol−1 for triflate, +2.8 cm3 mol−1 for Cl−) and ΔVCOUL⧧ (−4.2 cm3 mol−1) effectively cancel, giving ΔVex⧧(theor) = −10.3 cm3 mol−1 for Cl− as counteranion and −10.4 cm3 mol−1 for CF3SO3−. If, as suggested by Muzikár ̌ and Fawcett,23 the effective charge on Ru(NH3)63+ is only about +1, ΔVDH⧧ and ΔVCOUL⧧ will be +0.9 and −1.4 cm3 mol−1, respectively, and their net contribution will be within the experimental uncertainty, with ΔVex⧧(theor) = −9.4 cm3 mol−1 and ΔVel⧧(theor) = −4.7 cm3 mol−1. For a simple Ru(NH3)63+/2+ electrode reaction, then, the expectation is that ΔVel⧧(theor) (averaged over the 200 MPa pressure range) should be 0.5ΔVex⧧(theor) or about −5 cm3 mol−1, which is well within the range of observed ΔVel⧧ values for electrode reactions of metal ion complexes that do not involve large spin-state changes.1 The observed values of ΔVel⧧ for Ru(NH3)63+/2+, however, were −12 ± 1 cm3 mol−1 for 0.1 mol L−1 KCl and −16 ± 1 cm3 mol−1 for 0.1 mol L−1 KCF3SO3, which are the most negative ΔVel⧧ recorded to date for electrode reactions of transition-metal complexes in water. The only couples for which ΔVel⧧ has been found to approach these values are Co(en)33+/2+, Co(bpy)33+/2+, and Co(phen)33+/2+ (bpy = 2,2′-bipyridyl, phen = 1,10-phenanthroline),1 for which large distortions due to electronic spin state changes accompany the electron transfer process; such distortions are not expected to occur in the Ru(NH3)63+/2+ couple, in which both members are in low-spin 4d5/4d6 electronic configurations. In fact, we have shown above that the Ru(NH3)63+/2+ electrode reaction is not simple, being specifically catalyzed by anions, and that ΔVel⧧ is distinctly more negative for CF3SO3− than for Cl−. Ion pairing of Ru(NH3)63+ with the anion present might be invoked to explain the catalysis, and indeed Waysbort et al.93 gave evidence for about 30% pairing of Ru(NH3)63+ with Cl− in 0.1 mol L−1 aqueous chloride at 25 °C. The strongly negative ΔVel⧧, however, is not attributable to ion pairing because increasing pressure works against ion pairing by increasing the relative permittivity ε and also favoring hydration of the separated ionsfor example, the ion pair formation constant for {Ru(NH3)63+,Cl−}, calculated as per Fuoss,94 2765


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dominated by large solvational effects at the Ru ammine centers.102 In retrospect, even the puzzling strongly negative volumes of activation found for the aquation of Ru(NH3)5Cl2+ and its reverse could be understood in terms of solvation increases specific to activation processes in RuIII ammines.103,104 In short, there is ample precedent for specific hydrational interactions involving RuIII and RuII ammine complexes. There remains the possibility that the strongly negative ΔVel⧧ for the Ru(NH3)63+ reduction at an electrode reflects pressure effects on the electrical double layer. Experience with supporting electrolyte (KCl) concentration effects on the kinetics of the Fe(CN)63−/4− electrode reaction (Table 2),

a

kel/cm s−1 at 25 °C, P = 0.1 MPa

ΔVel⧧/cm3 mol−1

0.06 0.20 0.50

0.017 0.047 0.072

12.0 ± 1.8 10.4 ± 1.4 11.9 ± 1.3

CONCLUSIONS

Neither the rate constant kel nor the volume of activation ΔVel(obsd)⧧ for the reduction of Ru(NH3)63+ at a polycrystalline metallic UME depend significantly upon the identity of the metal, be it Au or Pt. According to traditional views,3,45 this is consistent with substantially full adiabaticity for the electron transfer process, but, as originally pointed out by Gosavi and Marcus,10 it does not preclude a modest level of nonadiabaticity. The question of the extent of nonadiabatic character is better pursued through adaptations of Marcus theory as proposed by Savéant6 and Compton;7,8 for the purposes of this study, the essential observation is that the kinetic parameters for reduction of Ru(NH3)63+ are independent of the choice of electrode material, Au vs Pt, within the experimental uncertainty. The apparent kel does, however, increase as the area of the UME decreases. Values of kel for the reduction of Ru(NH3)63+ depend strongly on the identity and concentration of the anion present in the order CF3SO3− < Cl− < ClO4−, but not upon the cation of the supporting electrolyte (Na+, K+, H+). For Cl− as the counterion of both Ru(NH3)63+ and the supporting electrolyte, kel is directly proportional to the total Cl− concentration, such that kel would be zero, within the experimental uncertainty, if Cl− were hypothetically absent. This result echoes (with charge reversal) the dependences of both kel and kex for many anion− anion electron transfer reactions on total cation concentrations, and suggests that Cl− is directly involved in mediation of the Ru(NH3)63+/2+ electron transfer. For triflate as the sole counterion, the dependence of kel on the total [CF3SO3−] is not linear, possibly because the blocking of the available electrode surface becomes dominant at high triflate concentrations. In experiments with a perchlorate as the supporting electrolyte, 15 mmol L−1 chloride or triflate was also present as the counterion of Ru(NH3)63+ because of risks in preparing its perchlorate salt, so that interpretation of the results was less clear-cut except that ClO4− was nevertheless associated with the fastest Ru(NH3)63+/2+ electrode reaction rates. No variablepressure experiments were conducted with ClO4− because the already fast reaction became too fast for accurate measurement at elevated pressures, and besides the likelihood that ClO4− would oxidize the Ru complexes over the longer time-scale of a pressure cycle is well recognized.47,48 A more orthodox explanation of the accelerating effect of added electrolytes might be the collapsing of the diffuse double layer by the supporting electrolyte, but it is evident that the relevant factor is the total concentration of the specific anion rather than of the supporting electrolyte. The observed ΔVel⧧ values for reduction of Ru(NH3)63+ at an electrode in presence of 0.115 mol L−1 Cl− or CF3SO3− are much more negative than predicted by a theory that has been successfully applied to other electrode reactions1 but which is not directly applicable in this case because of the specific involvement of the anions in promoting the electron transfer process. The strongly negative values of ΔVel⧧ probably reflect solvation increases peculiar to activation processes in reactions of RuIII/II am(m)ine complexes. These solvation effects may be amplified by involvement of the anion in the activation process. A further anion-specific contribution to ΔVel⧧ may be the promotion of desorption of surface-blocking Cl− or especially CF3SO3− from electrodes by applied pressure. Increase of the available electrode surface area through pressure-induced desorption of specifically adsorbed anions could also explain

Table 2. Dependence of kel and ΔVel⧧ for the Fe(CN)63−/4− Electrode Reaction at a Pt Electrodea [KCl]/mol L−1

Article

Data from Table 5 of ref 1.

however, has been that ΔVel⧧ is independent of the concentration of a particular supporting electrolyte within the experimental error (average ΔVel⧧ = 11.4 ± 0.9 cm3 mol−1) even though kel is strongly dependent on it (actually on [K+]). The implication is that, for Fe(CN)63−/4− at least, the reactants are in hard (i.e., effectively incompressible) contact with either the electrode surface or an inert adsorbed layer at the outer Helmholtz plane (OHP) and hence ΔVel⧧ is insensitive to double-layer effects. It is reasonable to expect the same to hold for the Ru(NH3)63+/2+ couple which, although of the opposite charge-type, shows a similar dependence of kel on the total counterion concentration. Finally, we may consider briefly how ΔVel⧧ might be affected if Ru(NH3)63+ were not in hard contact with the electrode or at the OHP but were moving freely within the diffuse double layer when reduction occurs. A Frumkin correction105 to be applied to the observed volume of activation ΔVel(obsd)⧧ may be estimated as outlined in the Supporting Information; the concept of the Frumkin correction has recently been discredited,106 but it serves to give an indication of the sign and order of magnitude of the effect. The key results are that the Frumkin correction to ΔVel(obsd)⧧ is zero at distance x = 0 (i.e., at hard contact of Ru(NH3)63+ with an adsorbed layer at the OHP) and at distances greater than about 8 nm, but at intermediate distances the correction is always negativethat is, it cannot explain the already strongly negative values of ΔVel⧧. For a reasonable φ value of ∼100 mV, and with the effective z set at +1,23 the greatest correction would be only about −1 cm3 mol−1 near x = 1.0 nm which is quite far out in terms of electron transfer probability. It may therefore be safely inferred that ΔVel⧧, unlike kel, is insensitive to double-layer effects (cf. Table 2), and that electron transfer may be treated as occurring with Ru(NH3)63+ either in contact at the OHP or close to it. Direct contact with the electrode, however, would result in expulsion of adsorbed water molecules and partial dehydration of Ru(NH3)63+, both of which would tend to make ΔVel(obsd)⧧ less negative than predicted. 2766


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the fact that ΔVel⧧ is about 4 cm3 mol−1 more negative for the triflate system than for the chloride, if indeed the bulky CF3SO3− ion is more strongly adsorbed than Cl− on Au and Pt at the Ru(NH3)63+/2+ formal potential as reported by Bockris et al.90a point that merits reinvestigation. Frumkin corrections for reduction of free Ru(NH3)63+ within the diffuse double layer would make ΔVel⧧ even more negative than is observed, although the corrections would be small. Conversely, the strongly negative ΔVel⧧ values are inconsistent with reduction of Ru(NH3)63+ in direct contact with the metallic electrode surface, which would entail substantial dehydration of both the electrode surface and Ru(NH3)63+ with consequent positive contributions to ΔVel⧧. Reduction of Ru(NH3)63+ can be regarded as taking place either in hard contact with adsorbed water at the OHP or close to it.

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ASSOCIATED CONTENT

S Supporting Information *

Plots of temperature dependence of kel in 0.1 mol L−1 KCl and dependences of kel on [Cl−] and [CF3SO3−]; pressure dependence of the Frumkin correction. This material is available free of charge via the Internet at http://pubs.acs.org.

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AUTHOR INFORMATION

Corresponding Author

*Phone: 403-220-5358. Fax: 403-289-9488. E-mail: swaddle@ ucalgary.ca. Present Address

† Karunya University, Karunya Nagar, Coimbatore, Tamilnadu, India 641114.

Notes

The authors declare no competing financial interest.

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ACKNOWLEDGMENTS We thank Profs. J. Lipkowski (University of Guelph) and I. J. Burgess (University of Saskatchewan) for discussions and provision of their unpublished data relating to triflate adsorption on Au electrodes, and the Natural Sciences and Engineering Research Council of Canada for financial support.

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Kinetics of Reduction of Aqueous Hexaammineruthenium(III) Ion at Pt

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